US2459082A - Filter - Google Patents

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US2459082A
US2459082A US604363A US60436345A US2459082A US 2459082 A US2459082 A US 2459082A US 604363 A US604363 A US 604363A US 60436345 A US60436345 A US 60436345A US 2459082 A US2459082 A US 2459082A
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compartment
slurry
filter
valve
shaft
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US604363A
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Mccaskell William
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    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D33/00—Filters with filtering elements which move during the filtering operation
    • B01D33/15—Filters with filtering elements which move during the filtering operation with rotary plane filtering surfaces
    • B01D33/21—Filters with filtering elements which move during the filtering operation with rotary plane filtering surfaces with hollow filtering discs transversely mounted on a hollow rotary shaft
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D29/00—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor
    • B01D29/11—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor with bag, cage, hose, tube, sleeve or like filtering elements
    • B01D29/31—Self-supporting filtering elements
    • B01D29/35—Self-supporting filtering elements arranged for outward flow filtration
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D29/00—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor
    • B01D29/62—Regenerating the filter material in the filter
    • B01D29/64—Regenerating the filter material in the filter by scrapers, brushes, nozzles, or the like, acting on the cake side of the filtering element
    • B01D29/6469—Regenerating the filter material in the filter by scrapers, brushes, nozzles, or the like, acting on the cake side of the filtering element scrapers
    • B01D29/6476—Regenerating the filter material in the filter by scrapers, brushes, nozzles, or the like, acting on the cake side of the filtering element scrapers with a rotary movement with respect to the filtering element
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D29/00—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor
    • B01D29/76—Handling the filter cake in the filter for purposes other than for regenerating
    • B01D29/80—Handling the filter cake in the filter for purposes other than for regenerating for drying
    • B01D29/82—Handling the filter cake in the filter for purposes other than for regenerating for drying by compression
    • B01D29/828—Handling the filter cake in the filter for purposes other than for regenerating for drying by compression using screws
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D33/00—Filters with filtering elements which move during the filtering operation
    • B01D33/35—Filters with filtering elements which move during the filtering operation with multiple filtering elements characterised by their mutual disposition
    • B01D33/37—Filters with filtering elements which move during the filtering operation with multiple filtering elements characterised by their mutual disposition in parallel connection
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D33/00—Filters with filtering elements which move during the filtering operation
    • B01D33/35—Filters with filtering elements which move during the filtering operation with multiple filtering elements characterised by their mutual disposition
    • B01D33/37—Filters with filtering elements which move during the filtering operation with multiple filtering elements characterised by their mutual disposition in parallel connection
    • B01D33/39—Filters with filtering elements which move during the filtering operation with multiple filtering elements characterised by their mutual disposition in parallel connection concentrically or coaxially
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D33/00—Filters with filtering elements which move during the filtering operation
    • B01D33/44—Regenerating the filter material in the filter
    • B01D33/46—Regenerating the filter material in the filter by scrapers, brushes nozzles or the like acting on the cake-side of the filtering element
    • B01D33/466—Regenerating the filter material in the filter by scrapers, brushes nozzles or the like acting on the cake-side of the filtering element scrapers
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D33/00—Filters with filtering elements which move during the filtering operation
    • B01D33/44—Regenerating the filter material in the filter
    • B01D33/52—Regenerating the filter material in the filter by forces created by movement of the filter element
    • B01D33/54—Regenerating the filter material in the filter by forces created by movement of the filter element involving vibrations
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D33/00—Filters with filtering elements which move during the filtering operation
    • B01D33/80—Accessories
    • B01D33/804—Accessories integrally combined with devices for controlling the filtration
    • B01D33/806—Accessories integrally combined with devices for controlling the filtration by flow measuring

Definitions

  • This invention relates to fillters of the pressure or vacuum variety and more particularly to an improved arrangement for handling slurrles having a low percentage of solids,
  • One of the objects of the present invention is to provide a unitary filter arrangement having a compartment for thickening the slurry before transfer to a second compartment wherein the dry filter cake may be removed in a convenient form. Another object is to provide means to control the flow of thickened slurry to the dry filter cake portion of the device.
  • Fig. 1 is an elevation view partially in section with a portion of the piping shown in schematic form.
  • Figure 2 is a fragmentary schematic view of one type of valve arrangement causing pulsation of the filter elements.
  • container III may have a shaft II passing therethrough supported in bearings I2 and I3 of conventional stufiing box construction.
  • the container III is divided into two compartments I4 and I5 by means of division plate I6, said division plate having a bearing and stuffing box arrangement I! therein for preventing the flow of slurry between the two compartments.
  • the shaft preferably has a plurality of leaf type filter elements shown diagrammatically at I8. A plurality of elements may be used because the slurry has but few solids and a high percentage of liquor.
  • the filter elements are connected through passages I9 in a conventionalmanner to I the valve box '20 suitablyheld-onthe end of the shaft.
  • Filtrate is removed from the interior of the leaf filters l8 through passages I9, valve box 20, and pipe 2i.
  • Pressurea'lso may be applied through pipe 2
  • eccentric 5I (Fig. 2) can be driven in some suitable manner from shaft I I such as by a spur gear placed on the shaft in any desired place.
  • Pipe 52 may be connected to a pressure source relative to chamber I4 and pipe 53 to a vacuum.
  • Three-way valve 54 is operable by means of eccentric 5
  • Pipe 55 is connected to inlet passage 56 in valve box 20 and passages III in shaft II are connectable by passages 51 with chamber 58 which extends circumferentially around the end of the shaft II.
  • Bypass openings 59 communicate with passage I9.
  • a blank sector 60 is provided in valve box 20 so as to close off one or more of passages 51 when bypass 59 is in registry with pipe connection 56.
  • shaft II revolves, alternate pressure and vacuum will be applied to the leaves through passage 56.
  • the shaft II may be rotated by means of worm wheel and gear arrangement 22.
  • An agitator blade arrangement 44 may be mounted on the filter elements so as to keep the cake from filling up in the bottom of compartment I4.
  • a ball float 25 can be used to operate switch 26 for control of solenoid 21 of threeway valve 28.
  • Suction pump 29 is connected on the suction side through pipe 30 to supply tank 46.
  • Pipe 32 from three-way valve -28 is used to form a path for the slurry from pump '29 to thickener compartment I4.
  • from the threeway valve serves as a return to recirculate the slurry back to supply tank 46.
  • float valve 25 When float valve 25 lowers, it operates solenoid 21 in such a manner as to turn three-way valve 28 to supply slurry from supply tank 46 to thickener compartment I4.
  • float valve 25 operates three-way valve 28 to return slurry through pipe 3i back to the supply tank 46.
  • Float control is connected by means of electrical connections 6I to solenoid .23.
  • solenoid .23 When'flo'at 45 is. in a raised position due to the level in comthe control valve 48 so that slurry will be recirculated back to compartment I 4.
  • float 45 When liquid level incompartment I5 lowers, float 45 will be lowered to operate three-way valve 48 to conduct thickened slurry or liquid from compartment I4 through outlet pipe 49, pump 4?, outlet through level is reached in compartment I5,- float valve-45 will operate solenoid 23 and three-way valve 48 I5.
  • solenoid 23 When the proper a rtment I 5, solenoid 23 will be actuated to turn to recirculate slurry from outlet 50 of pump 41 back to slurry thickener compartment l4 through pipe 5
  • a single row leaf filter 33 may be mounted on shaft H in compartment l5 as indicated, said filter having conventional scraper plates 34 for scraping filter cake from the filter element.
  • Leaf 33 may also be of a drum type construction. Passages 35 in shaft ll lead from the interior of the leaf filter elements 33 to valve box 36, and pipe 31.
  • the filter cake, which is scraped from filter elements 33, is relatively dry and falls to the bottom of the container and can be removed by screw 38 to valve 39 where it passes to outlet 40 in a relatively dry cake form.
  • Motor drive 4! can be employed to operate shaft 42 which drives screw 38 and agitator blades 43.
  • slurry having a low percentage of solids is supplied to the slurry thickening compartment l4 wherein filtrate is removed through pipe 2
  • Pump 29 will feed slurry to compartment I4 until fioat '25 is raised by the level therein whereupon solenoid 21 will be actuated to operate valve 28 and recirculate slurry to supply tank 46.
  • Pump 41 will feed thickened slurry from compartment I4 to compartment I5 as fioat 45 is in its lowermost position. Filter element 33 will allow removal of filtrate through pipe 31 and filter cake will fall to the bottom of the compartment. Screw 38 will then remove the comparatively dry filter cake through valve 39.
  • a filter of the class described comprising a closed container rotating means connected to said shaft for rotating the same having two separated and closed compartments, a shaft extendin therethrough, a slurry thickener in one compartment of said container including filter means mounted on said shaft, means to withdraw filtrate'from said compartment through said shaft and filter, a second filter mounted on said shaft in a second compartment, means to transfer thickened slurry from said first compartment to said second compartment, means to remove filtrate from said second filter through said shaft, and means to remove filter cake from said second compartment.
  • a filter of the class described comprising a container having two compartments, a slurry thickener in one compartment of said container including filtering means, means to withdraw filtrate from said filter, filter means in a second compartment, means to transfer thickened slurry from said first compartment to said second compartment, level control means in said second compartment connected to said means to transfer thickened slurry to feed thickened slurry from said first compartment to said second compartment when the level of slurry in said compartment reaches a predetermined level, means to remove filtrate from said second filter, and means to remove filter cake from said second compartment.
  • a filter of the class described comprising a container having two compartments, a slurry thickener in one compartment including filtering means, filtrate being passable through said thickener, filter means in a second compartment, means to transfer thickened slurry from said first compartment through said thickener to said second compartment including a pump with an inlet connected to said first compartment, a three-way valve selectively connecting the outlet of said pump to said first and second compartments, and control means in said second compartment for operating said valve to transfer slurry from said first compartment to said second compartment when the slurry therein is below a predetermined level.
  • a filter of the class described comprising a container having two compartments, a slurry thickener in one compartment of said container including filtering means, filtrate being passable through said thickener, means to withdraw filtrate from said compartment through said thickener, filter means in a second compartment, means to transfer thickened slurry from said first compartment to said second compartment including a pump with an inlet connected to said first compartment, valve means selectively connecting the outlet of said pump to said first and second compartments, a supply tank, a second pump having the inlet thereof connected to said tank, second valve means selectively connecting the outlet of said pump to said slurry thickener compartment and to said supply tank, and float control means in said slurry thickener compartment to control said second valve.
  • a filter of the class described comprising a container having two compartments, a shaft passing therethrough, a slurry thickener in one compartment of said container including a plurality of leaf filter elements mounted on said shaft, means to withdraw filtrate from said filter elements through said shaft, means to pulsate said filter elements, a leaf filter mounted on said shaft in a second compartment of said container, a slurry pump connected to said first compartment, a three-way valve in the outlet of said pump for transferring slurry to said second compartment and for returning it to said first compartment, level control means in said second compartment for operating said three-way valve to cause transfer of thickened slurry from said first compartment to said second compartment when the level of slurry in said second compartment reaches a predetermined level, means to remove filtrate from said second leaf filter, and screw conveyor means to remove filter cake from the bottom of said second compartment.

Description

Jan. 11, 1949. w MGCASKELL FILTER Filed July 11' 1945 4 TTOPNE Y5 filter cake,
Patented Jan. 11, 1949 UNITED STATES PATENT OFFICE 9 Claims.
This invention relates to fillters of the pressure or vacuum variety and more particularly to an improved arrangement for handling slurrles having a low percentage of solids,
In order to obtain efficient operation of leaf type filters, such as disclosed in Patent No. 1,266,- 133 issued May 14, 1918, or in Patent No. 1,259,139 it is desirable that there be a certain amount of filter cake on the surface of the filter elements. When filtering a substance such as a refined cottonseed oil, which has only 2 /2% clay or other solid material, considerable time is required to build up a cake sufficient to obtain efficient operation.
One of the objects of the present invention is to provide a unitary filter arrangement having a compartment for thickening the slurry before transfer to a second compartment wherein the dry filter cake may be removed in a convenient form. Another object is to provide means to control the flow of thickened slurry to the dry filter cake portion of the device. These and other objects of the invention will become apparent from the following description and drawings which are merely exemplary.
In the drawings:
Fig. 1 is an elevation view partially in section with a portion of the piping shown in schematic form.
Figure 2 is a fragmentary schematic view of one type of valve arrangement causing pulsation of the filter elements.
In the preferred form shown, container III may have a shaft II passing therethrough supported in bearings I2 and I3 of conventional stufiing box construction. The container III is divided into two compartments I4 and I5 by means of division plate I6, said division plate having a bearing and stuffing box arrangement I! therein for preventing the flow of slurry between the two compartments. In the slurry thickenin compartment I4, the shaft preferably has a plurality of leaf type filter elements shown diagrammatically at I8. A plurality of elements may be used because the slurry has but few solids and a high percentage of liquor. The filter elements are connected through passages I9 in a conventionalmanner to I the valve box '20 suitablyheld-onthe end of the shaft. Filtrate is removed from the interior of the leaf filters l8 through passages I9, valve box 20, and pipe 2i. Pressurea'lso may be applied through pipe 2|, or by a suitable valve arrange-' -ment, to the interior of the filter element'so as to cause pulsation thereof to remove the formed such as seen in'Patent No. 1,700,772
inlet 32' to compartment or Patent No. 1,835,796. As an example of one manner of causing pulsation of the filter elements, eccentric 5I (Fig. 2) can be driven in some suitable manner from shaft I I such as by a spur gear placed on the shaft in any desired place. Pipe 52 may be connected to a pressure source relative to chamber I4 and pipe 53 to a vacuum. Three-way valve 54 is operable by means of eccentric 5| to alternately connect pipe 55 with pres- .sure pipe 52 and vacuum pipe 53. Pipe 55 is connected to inlet passage 56 in valve box 20 and passages III in shaft II are connectable by passages 51 with chamber 58 which extends circumferentially around the end of the shaft II. Bypass openings 59 communicate with passage I9. A blank sector 60 is provided in valve box 20 so as to close off one or more of passages 51 when bypass 59 is in registry with pipe connection 56. As shaft II revolves, alternate pressure and vacuum will be applied to the leaves through passage 56. The shaft II may be rotated by means of worm wheel and gear arrangement 22. An agitator blade arrangement 44 may be mounted on the filter elements so as to keep the cake from filling up in the bottom of compartment I4.
In dome 24, a ball float 25 can be used to operate switch 26 for control of solenoid 21 of threeway valve 28. Suction pump 29 is connected on the suction side through pipe 30 to supply tank 46. Pipe 32 from three-way valve -28 is used to form a path for the slurry from pump '29 to thickener compartment I4. Pipe 3| from the threeway valve serves as a return to recirculate the slurry back to supply tank 46. When float valve 25 lowers, it operates solenoid 21 in such a manner as to turn three-way valve 28 to supply slurry from supply tank 46 to thickener compartment I4. -As.the level rises in compartment I4, float valve 25 operates three-way valve 28 to return slurry through pipe 3i back to the supply tank 46.
Float control is connected by means of electrical connections 6I to solenoid .23. When'flo'at 45 is. in a raised position due to the level in comthe control valve 48 so that slurry will be recirculated back to compartment I 4. When liquid level incompartment I5 lowers, float 45 will be lowered to operate three-way valve 48 to conduct thickened slurry or liquid from compartment I4 through outlet pipe 49, pump 4?, outlet through level is reached in compartment I5,- float valve-45 will operate solenoid 23 and three-way valve 48 I5. When the proper a rtment I 5, solenoid 23 will be actuated to turn to recirculate slurry from outlet 50 of pump 41 back to slurry thickener compartment l4 through pipe 5|.
A single row leaf filter 33 may be mounted on shaft H in compartment l5 as indicated, said filter having conventional scraper plates 34 for scraping filter cake from the filter element. Leaf 33 may also be of a drum type construction. Passages 35 in shaft ll lead from the interior of the leaf filter elements 33 to valve box 36, and pipe 31. The filter cake, which is scraped from filter elements 33, is relatively dry and falls to the bottom of the container and can be removed by screw 38 to valve 39 where it passes to outlet 40 in a relatively dry cake form. Motor drive 4! can be employed to operate shaft 42 which drives screw 38 and agitator blades 43.
Summarizing the operation, slurry having a low percentage of solids is supplied to the slurry thickening compartment l4 wherein filtrate is removed through pipe 2|, pressure pulsations being applied to the filter elements, if desired, in order to remove at least some of the sludge or cake thereon. Pump 29 will feed slurry to compartment I4 until fioat '25 is raised by the level therein whereupon solenoid 21 will be actuated to operate valve 28 and recirculate slurry to supply tank 46. Pump 41 will feed thickened slurry from compartment I4 to compartment I5 as fioat 45 is in its lowermost position. Filter element 33 will allow removal of filtrate through pipe 31 and filter cake will fall to the bottom of the compartment. Screw 38 will then remove the comparatively dry filter cake through valve 39.
Various modifications of the invention may be made without departing from the spirit of the invention or the scope thereof as defined in the appended claims.
I claim:
1. In a filter of the class described, the combination comprising a closed container rotating means connected to said shaft for rotating the same having two separated and closed compartments, a shaft extendin therethrough, a slurry thickener in one compartment of said container including filter means mounted on said shaft, means to withdraw filtrate'from said compartment through said shaft and filter, a second filter mounted on said shaft in a second compartment, means to transfer thickened slurry from said first compartment to said second compartment, means to remove filtrate from said second filter through said shaft, and means to remove filter cake from said second compartment.
2. In a filter of the class described, the combination comprising a container having two compartments, a slurry thickener in one compartment of said container including filtering means, means to withdraw filtrate from said filter, filter means in a second compartment, means to transfer thickened slurry from said first compartment to said second compartment, level control means in said second compartment connected to said means to transfer thickened slurry to feed thickened slurry from said first compartment to said second compartment when the level of slurry in said compartment reaches a predetermined level, means to remove filtrate from said second filter, and means to remove filter cake from said second compartment.
3. In-a filter of the class described, the combination comprising a container having two compartments, a, slurry thickener in one compartment of said container including filtering moans, filtrate being passable through said with an inlet connected to said first compartment, and valve means selectively connecting the outlet of said pump to said first and second compartments.
4. In a filter of the class described, the combination comprising a container having two compartments, a slurry thickener in one compartment including filtering means, filtrate being passable through said thickener, filter means in a second compartment, means to transfer thickened slurry from said first compartment through said thickener to said second compartment including a pump with an inlet connected to said first compartment, a three-way valve selectively connecting the outlet of said pump to said first and second compartments, and control means in said second compartment for operating said valve to transfer slurry from said first compartment to said second compartment when the slurry therein is below a predetermined level.
5. In a filter of the class described, the combination comprising a container having two compartments, a slurry thickener in one compartment of said container including a filterin means, means to withdraw filtrate from said filter, a leaf filter means in a second compartment, and means to transfer thickened slurry from said first compartment to said second compartment including a three-way valve, float means in said second compartment for controlling said valve to transfer thickened slurry to said second compartment when the slurry therein is below a predetermined level. i
6. In a filter of the class described, the combination comprising a container having two compartments, a slurry thickener in one compartment of said container including filtering means, filtrate being passable through said thickener, means to withdraw filtrate from said compartment through said thickener, filter means in a second compartment, means to transfer thickened slurry from said first compartment to said second compartment includin a pump with an inlet connected to said first compartment, valve means selectively connecting the outlet of said pump to said first and second compartments, and means for supplying and controlling the level of slurry in said slurry thickener.
'7. In a filter of the class described, the combination comprising a container having two compartments, a slurry thickener in one compartment of said container including filtering means, filtrate being passable through said thickener, means to withdraw filtrate from said compartment through said thickener, filter means in a second compartment, means to transfer thickened slurry from said first compartment to said second compartment including a pump with an inlet connected to said first compartment, valve means selectively connecting the outlet of said pump to said first and second compartments, a supply tank, a second pump having the inlet thereof connected to said tank, second valve means selectively connecting the outlet of said pump to said slurry thickener compartment and to said supply tank, and float control means in said slurry thickener compartment to control said second valve.
8. In a filter of the class described, the combination comprising a container having two compartments, a shaft passing therethrough, a slurry thickener in one compartment of said container including a plurality of leaf filter elements mounted on said shaft, means to withdraw filtrate from said filter elements through said shaft, means to pulsate said filter elements, a leaf filter mounted on said shaft in a second compartment of said container, a slurry pump connected to said first compartment, a three-way valve in the outlet of said pump for transferring slurry to said second compartment and for returning it to said first compartment, level control means in said second compartment for operating said three-way valve to cause transfer of thickened slurry from said first compartment to said second compartment when the level of slurry in said second compartment reaches a predetermined level, means to remove filtrate from said second leaf filter, and screw conveyor means to remove filter cake from the bottom of said second compartment.
9. In a unitary filter of the class described, the combination comprising a closed container having two closed compartments, a slurry thickener including filtering means in a first com- REFERENCES CITED The following references are of record in the file of this patent:
UNITED STATES PATENTS Number Name Date 1,494,122 McCaskell Ma 13, 1924 1,835,796 McCaskell Dec. 8, 1931 FOREIGN PATENTS Number Country Date Germany Sept. 20, 1928
US604363A 1945-07-11 1945-07-11 Filter Expired - Lifetime US2459082A (en)

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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE1253675B (en) * 1960-03-14 1967-11-09 Gene Hirs Filter device for liquids
DE1259842B (en) * 1960-06-29 1968-02-01 Laval Turbine Bag filter
US4521312A (en) * 1982-05-03 1985-06-04 Anderson Edward M Apparatus and method for separating a mixture of three liquids
US11000791B2 (en) * 2019-03-06 2021-05-11 Veolia Water Solutions & Technologies Support Rotary disc filter having backwash guides

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1494122A (en) * 1923-06-20 1924-05-13 Jasper A Mccaskell Filter
DE465615C (en) * 1924-10-22 1928-09-20 Foelsche Fa R Device for filtering thin liquid slimes by means of vacuum cell filters connected in series
US1835796A (en) * 1931-12-08 mccaskell

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1835796A (en) * 1931-12-08 mccaskell
US1494122A (en) * 1923-06-20 1924-05-13 Jasper A Mccaskell Filter
DE465615C (en) * 1924-10-22 1928-09-20 Foelsche Fa R Device for filtering thin liquid slimes by means of vacuum cell filters connected in series

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE1253675B (en) * 1960-03-14 1967-11-09 Gene Hirs Filter device for liquids
DE1259842B (en) * 1960-06-29 1968-02-01 Laval Turbine Bag filter
US4521312A (en) * 1982-05-03 1985-06-04 Anderson Edward M Apparatus and method for separating a mixture of three liquids
US11000791B2 (en) * 2019-03-06 2021-05-11 Veolia Water Solutions & Technologies Support Rotary disc filter having backwash guides

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